Irrigation with domestic wastewater: a multivariate analysis of main soil changes

Irrigation with treated domestic sewage wastewater (TSE) is an agricultural practice to reduce water requirements of agroecossystems and the nutrient load impact on freshwaters, but adverse effects on soil chemical (salinization, sodification, etc.) and soil physical properties (alteration in soil porosity and hydraulic conductivity, etc.) have been reported. This study aimed to define some relationships among these changes in an Oxisol using multivariate analysis. Corn (Zea mays L.) and sunflower (Helianthus annuus L.) were grown for two years, irrigated with TSE. The following soil properties were determined: Ca2+; Mg2+; Na+; K+ and H + Al contents, cationic exchangeable capacity (CEC), sum of bases (SB), base saturation (V), texture (sand, silt and clay), macro-, micro-, and cryptoporosity (V MA, V MI and V CRI), water content at soil saturation (θS) and at field capacity (θFC), residual water content (θR), soil bulk density (d s), water dispersed clay (WDC) and saturated hydraulic conductivity (K SAT). Factor analysis revealed the following six principal factors: Fine Porosity (composed of Na+; K+; WDC, θR, θRFC, and V CRI); Large Porosity (θS, d s, V MA, Vs); Soil CEC (Ca2+; Mg2+; CEC, SB, V); Soil Acidity (H + Al); and Soil Texture (factors 5 and 6). A dual pore structure appears clearly to the factors 1 and 2, with an apparent relationship between fine porosity and the monovalent cations Na+ and K+. The irrigation (with potable sodic tap water or sewage wastewater) only had a significant effect on Fine Porosity and Large Porosity factors, while factors 3 and 4 (Soil CEC and Soil Acidity) were correlated with soil depth. The main conclusion was a shift in pore distribution (large to fine pores) during irrigation with TSE, which induces an increase of water storage and reduces the capacity of drainage of salts.

Industrial-Scale hydrothermal carbonization of waste sludge materials for fuel production

Hydrothermal carbonization (HTC) is a thermochemical process used in the production of charred matter similar in composition to coal. It involves the use of wet, carbohydrate feedstock, a relatively low temperature environment (180 °C-350 °C) and high autogenous pressure (up to 2,4 MPa) in a closed system. Various applications of the solid char product exist, opening the way for a range of biomass feedstock materials to be exploited that have so far proven to be troublesome due to high water content or other factors. Sludge materials are investigated as candidates for industrial-scale HTC treatment in fuel production. In general, HTC treatment of pulp and paper industry sludge (PPS) and anaerobically digested municipal sewage sludge (ADS) using existing technology is competitive with traditional treatment options, which range in price from EUR 30-80 per ton of wet sludge. PPS and ADS can be treated by HTC for less than EUR 13 and 33, respectively. Opportunities and challenges related to HTC exist, as this relatively new technology moves from laboratory and pilot-scale production to an industrial scale. Feedstock materials, end-products, process conditions and local markets ultimately determine the feasibility of a given HTC operation. However, there is potential for sludge materials to be converted to sustainable bio-coal fuel in a Finnish context.

Eliminación de compuestos causantes de olores mediante adsorbentes/catalizadores obtenidos a partir de lodos de depuradora

El aumento de la cantidad de lodos y las dificultades inherentes a su aplicación agrícola y/o disposición en vertederos, hace necesario encontrar nuevas alternativas para su gestión. A nivel europeo, hoy en día se tiende hacia la aplicación de tratamientos térmicos (incineración, pirólisis y gasificación) que permiten una valoración energética de los lodos, si bien generan un residuo sólido que sigue siendo necesario gestionar. El problema medioambiental provocado por (malos) olores resulta difícil de abordar de una manera genérica, teniendo en consideración la propia naturaleza del olor y sus posibles causas. Los olores en las EDARs son provocados básicamente por la degradación de la materia orgánica en condiciones anaeróbicas y se detectan en todas las operaciones unitarias en diferentes niveles de concentración. Esta tesis incidiendo en ambos aspectos, tiene por objeto investigar la valorización de lodos como materiales precursores de adsorbentes/ catalizadores para la eliminación de olores en el entorno de las EDARs, maximizando la reutilización de los lodos. Para la realización de los experimentos se han seleccionado lodos procedentes de tres EDARs situadas en la región de Girona (SC, SB, SL) que difieren en cuanto al tratamiento de los lodos. Ambas muestras han sido caracterizadas con el fin de determinar las diferencias más importantes en los lodos de partida. Los parámetros de caracterización incluyen el análisis de composición química (análisis elemental e inmediato, determinación contenido en cenizas, medida pH, DRX, FT-IR, SEM / EDX) así como análisis de superficie (adsorción de N2 y CO2). En primer lugar los lodos caracterizados han sido sometidos a diferentes tratamientos térmicos de gasificación y pirólisis y los adsorbentes/ catalizadores obtenidos se han probado como adsorbentes para la eliminación de H2S. Como consecuencia de este estudio, se ha desechado el uso de uno de lodos (SC) puesto que se obtenían resultados muy similares a (SB), a continuación el estudio se centró en el lodo de SL. Con este objetivo se han preparado 12 muestras 6 de ellas pirolizadas y 6 gasificadas en el rango de temperaturas que comprende 600-1100 ºC. Posteriormente las muestras han sido caracterizadas y se ha determinado la capacidad de eliminación (x/M) del H2S. Los resultados muestran que hemos sido capaces de obtener unos materiales que si bien, presentan un bajo desarrollo de porosidad dan lugar a valores de capacidades de eliminación elevados y comparables a carbones y materiales adsorbentes comerciales (Centaur, Sorbalit). Las elevadas eficiencias de eliminación se atribuyen básicamente a la presencia de especies catalíticamente activas tales como los óxidos mixtos de calcio y hierro determinados por DRX en las muestras tratadas térmicamente. El segundo bloque de resultados se centra la mejora de las propiedades texturales de estos materiales adsorbentes. Con este objetivo se llevaron acabo procesos de activación física con CO2 y química con H3PO4 e hidróxidos alcalinos (NaOH y KOH), que hasta el momento no se había probado con este tipo de precursores. Los resultados indican que la activación física (CO2) y química (H3PO4) no son unos buenos métodos para la obtención de adsorbentes altamente porosos con este tipo de materia prima bajo las condiciones probadas, sin embargo la activación con hidróxidos alcalinos da lugar a materiales adsorbentes con superficies específicas de hasta 1600 m2g-1. En el caso de la activación con hidróxidos, tanto el incremento de la relación agente activante/ precursor como el incremento de la temperatura producen un descenso del rendimiento, al mismo tiempo que incrementan el valor de SBET. Los materiales resultantes de la activación con hidróxidos alcalinos se han probado como adsorbentes/ catalizadores para la eliminación de H2S. Los resultados indican que un incremento del área superficial no es indicativo de un aumento de la capacidad de eliminación dada la naturaleza ácida de estos materiales obtenidos. Con el fin de contrarrestar el efecto ácido de estos materiales se han realizado los mismos ensayos añadiendo NaOH al lecho de reacción llegando a valores de x/M de hasta 450 mgg-1. Posteriormente también se han realizado ensayos de eliminación de NH3 con algunas de estas muestras, y los resultados obtenidos de x/M son del orden de carbones activados comerciales. Los materiales adsorbentes obtenidos tras la activación con hidróxidos alcalinos se convierten en materiales muy atractivos para ser utilizados como adsorbentes/ catalizadores de múltiples contaminantes (COVs, Hg...).

Degradation and plant uptake of nonylphenol (NP) and nonylphenol-12-ethoxylate (NP12EO) in four contrasting agricultural soils

Nonylphenol polyethoxylates (NPEOs) are surfactants found ubiquitously in the environment due to widespread industrial and domestic use. Biodegradation of NPEOs produces nonylphenol (NP), an endocrine disruptor. Sewage sludge application introduces NPEOs and NP into soils, potentially leading to accumulation in soils and crops. We examined degradation of NP and nonyl phenol-12-ethoxylate (NP12EO) in four soils. NP12EO degraded rapidly (initial half time 0.3-5 days). Concentrations became undetectable within 70-90 days, with a small increase in NP concentrations after 30 days. NP initially degraded quickly (mean half time 11.5 days), but in three soils a recalcitrant fraction of 26-35% remained: the non-degrading fraction may consist of branched isomers, resistant to biodegradation. Uptake of NP by bean plants was also examined. Mean bioconcentration factors for shoots and seeds were 0.71 and 0.58, respectively. Removal of NP from the soil by plant uptake was negligible (0.01-0.02% of initial NP). Root concentrations were substantially higher than shoot and seed concentrations. (C) 2008 Elsevier Ltd. All rights reserved.

Comportamento do reator seqüencial em batelada (RSB) sob estado estacionário dinâmico utilizando idade do lodo como parâmetro de controle operacional

O reator seqüencial em batelada (RSB) é uma variante de lodos ativados capaz de promover a remoção da matéria orgânica, a remoção dos nutrientes e a separação da fase sólida da líquida em uma unidade. A valorização das áreas urbanas, a carência de tratamento terciário e a crescente necessidade de redução nas dimensões de estações de tratamento de esgoto devem impulsionar o desenvolvimento de pesquisas sobre RSB em curto espaço de tempo. A partir deste cenário, o presente trabalho teve como objetivo modelar o comportamento do reator seqüencial em batelada a partir da teoria desenvolvida por Marais e colaboradores. Dentro deste contexto, a cinética de oxidação dos compostos orgânicos e do nitrogênio na forma amoniacal foi descrita e modelada. O trabalho experimental foi realizado em duas escalas: bancada e piloto. O experimento em escala de bancada foi dividido em duas fases. Foram utilizados dois RSBs e um sistema de fluxo contínuo. Um reator seqüencial em batelada (RSB1) foi operado com idade de lodo. O outro reator em batelada (RSB2) foi operado em função da relação F/M e o sistema de fluxo contínuo (FC1) por idade de lodo. Estes reatores foram utilizados como controle no monitoramento do RSB1 Na primeira fase, os três sistemas removeram apenas matéria orgânica. Na fase seguinte, removeram matéria orgânica e nitrogênio. A partir dos resultados obtidos em escala de bancada, foi possível concluir que o modelo desenvolvido pode ser aplicado ao reator seqüencial em batelada operando com idade de lodo, permitindo determinar a qualidade do efluente, a produção de lodo e o consumo de oxidante. Além disso, foi possível descrever o comportamento da taxa de consumo de oxigênio em função da oxidação da matéria orgânica biodegradável e da oxidação do nitrogênio na forma amoniacal. O reator seqüencial em batelada operado com idade de lodo (RSB1) alcançou remoção média de matéria orgânica de 90 % nas idades de lodo de 30, 20, 10 e 5 dias. A remoção média de nitrogênio mais elevada foi obtida na idade de lodo de 20 dias e atingiu 87 %. Nas demais idades de lodo a remoção média de nitrogênio variou entre 79 e 42 %. A modelagem do comportamento do reator seqüencial em batelada resultou numa proposta de metodologia para o dimensionamento que tem como finalidade abolir critérios obsoletos e inadequados para o dimensionamento de lodos ativados em batelada No experimento em escala piloto, foram utilizados um reator seqüencial em batelada, denominado RSB, e um sistema de fluxo contínuo com a configuração Bardenpho, denominado FC. Os sistemas de lodos ativados sob investigação foram monitorados em duas idades de lodo: 30 e 10 dias. Os dados do experimento em escala piloto mostraram que os processos físico-químicos e biológicos envolvidos na remoção de matéria orgânica e nitrogênio no RSB foram mais eficientes do que no Bardenpho quando trataram o mesmo esgoto doméstico e foram submetidos às mesmas condições operacionais. No RSB, obteve-se 88 e 89 % de remoção de matéria orgânica nas idades de lodo de 10 e 30 dias, respectivamente. Nesta seqüência das idades de lodo, a eficiência do Bardenpho caiu de 87 para 76 %. O sistema de fluxo contínuo removeu 66 e 52 % do nitrogênio total afluente nas idades de lodo de 10 e 30 dias, respectivamente. A eficiência do RSB na remoção de nitrogênio foi determinada apenas na idade de lodo de 10 dias e alcançou 69 %. A partir dos resultados obtidos em escala de bancada e piloto, constata-se que o reator seqüencial em batelada operando com idade de lodo pode ser utilizado no tratamento de esgoto doméstico e obter eficiência na remoção de matéria orgânica e nitrogênio igual ou superior ao sistema de fluxo contínuo.

Atributos físicos de Latossolos adubados durante cinco anos com biossólido

A utilização do biossólido para fins agrícolas tem sido uma alternativa viável para resíduos de origem domiciliar e industrial. O objetivo deste trabalho foi avaliar o efeito da aplicação de biossólido nos atributos físicos de Latossolo Vermelho distrófico, textura média (LVd), e Latossolo Vermelho eutroférrico argiloso (LVef). Utilizaram-se as doses, acumuladas em 5 anos, de 0,0, 25,0, 47,5 e 50,0 Mg ha-1 de matéria seca de biossólido, incorporadas até 0,1 m com grade. As amostras deformadas foram coletadas no quinto ano, após a colheita do milho, nas camadas de 0,0-0,1, de 0,1-0,2 e de 0,2-0,3 m para determinação da composição granulométrica e matéria orgânica. As amostras indeformadas coletadas com cilindros metálicos de 0,030 m de altura e 0,048 m de diâmetro, também no quinto ano, foram utilizadas para determinação da densidade, porosidade e retenção de água no solo. A macroporosidade foi superior a partir de 47,5 Mg ha-1 e 50,0 Mg ha-1 de biossólido, no LVd e LVef, respectivamente, e a densidade do solo foi inferior na dose de 50,0 Mg ha-1 no LVd de textura média, na camada de 0,0-0,1 m. A aplicação de 50,0 Mg ha-1 de biossólido não alterou a porosidade total, a microporosidade e a retenção de água nos dois solos. O efeito da aplicação do biossólido depende do tipo de solo e da quantidade aplicada.

Nitrificação de efluentes de reatores anaeróbicos em filtros submersos aerados

Although the good performance in organic matter and suspended solids removal, the anaerobic reactors are unable to remove ammonia nitrogen from sewage, which makes indispensable to include a step of post-treatment for removal of ammonia or nitrate as necessary. This paper presents the performance of a new variant technology, where the nitrification unit, preceded by anaerobic units, is a submerged aerated biological filter, without continuous sludge discharge in their daily operation. The oxygenation system is very simple and inexpensive, consisting of perforated hoses and compressors. The anaerobic reactors are a septic tank with two chambers followed (8.82 m³) and two parallel anaerobic filters (36 m³ each) filled with ceramic bricks and conics plastic parts. Both followed aerated filters were filled with cut corrugated conduit. The study evaluated the behavior of the system with constant domestic sewage flow (10 m³/d) and different aeration conditions, are these: stage 01, when applied air flow of 0.01 m³ air/min in both aerated filter; stage 02, remained in the initial air flow rate in the second aerated filter and increased at the first to 0.05 m³ air/min; at last, at last, in stage 03, the air flow rate of first aerated filter was 0.10 m³ air/min and on the second remained at 0.01 m³ air/min. The filter FA1 received load of 0.41 kg COD/m³.d, 0.37 kg COD/m³.d and 0.26 kg COD/m³.d on phases 01, 02 and 03, respectively. The FA2 received loads of 0.25 kg COD/m³.d, 0.18 kg COD/m³.d and 0.14 kg COD/m³.d on phases 01, 02 and 03, respectively. During stage 01, were found the following results: 98% removals of BODtotal and 92% of CODtotal, with effluent presenting 9 mg/L of BODtotal final average and 53 mg/L of CODtotal average; suspended solids removals of 93%, with a mean concentration of 10 mg/L in the final effluent; 47% reduction of ammonia of FA2 to FAN 's, presenting average of 28 mg NNH3/ L of ammonia in the effluent with; the dissolved oxygen levels always remained around 2.0 mg/L. During stage 02, were found removals of 97% and 95% to BODtotal and suspended solids, respectively, with average final concentrations of 8 and 7 mg/L, respectively; was removed 60% of ammonia, whose final concentration was 16.3 mg NNH3/ L, and nitrate was increased to a final average concentration of 16.55 mg N-NO3/L. Finally, the stage 03 provided 6 mg/L of DBOtotal (98% removal) and 23 mg/L of CODtotal (95% removal) of final effluent concentrations average. At this stage was identified the higher ammonia oxidation (86%), with final effluent showing average concentration of 6.1 mg N-NH3/L, reaching a minimum of 1.70 mg N-NH3/L. In some moments, during stage 03, there was a moderate denitrification process in the last aerated filter. The average turbidity in the effluent showed around 1.5 NTU, proving the good biomass physical stability. Therefore, the results demonstrate the submerged biological filters potential, filled with high void ratio material (98%), and aerated with hoses and compressor adoption, in the carbonaceous and nitrogenous matter oxidation, also generating an effluent with low concentration of solids

Avaliação da eficiência da remoção de matéria orgânica e microbiológica de três sistemas de lagoas de estabilização em série na Grande Natal-RN: Beira Rio, Jardim Lola I e Jardim Lola II

Waste stabilization ponds are the main technology in use for domestic sewage treatment in Rio Grande do Norte State (RN), northeast Brazil. The are around 80 systems, constructed mainly by municipal city halls, being series comprised by a primary facultative pond followed by two maturation ponds the most used configuration. Due to problems related with the production and destination of sludge and generation of bad odors, the designers have avoided the use of anaerobic lagoons. The majority of systems are rarely monitored to verify their efficiencies and to get new project parameters for future designing. This work has as purpose to make a diagnosis of efficiency of three series of waste stabilization pond series (WSPS) of Jardim Lola 1, Jardim Lola 2 and Beira Rio, located in the North Zone of the city of the Natal/RN, treating domestic raw sewage, on the removal of organic matter and thermotolerant coliform, comparing the operational conditions of the systems this inside of the bands foreseen in the project, through parameters BOD5, QOD, thermotolerant coliforms, dissolved oxygen, pH, temperature, ammoniac nitrogen, total and suspended solids. The work was carried through in the WSPS, all constituted by a primary facultative pond followed by two maturation ponds. Socioeconomic characteristics of population are predominantly low and all the plants are very near of the contributing basins. The series were monitored from of May the November of 2002, totalizing 20 collections of grab samples of raw sewage and ponds effluents between 8:00 and 9:50 h. The main aspect to be detached by the results was the great concentration of organic matter (BOD and COD) and microorganisms the raw sewage which were around two times more concentrated than those values foreseen one in project. Considering all series the highest removals of organic matter were observed in system Beira Rio (84 and 78% of BOD and COD, respectively), which presented high hydraulic detention time (TDH = 89 days). On the other hand, Jardim Lola 1 and Jardim Lola 2 presented a much lower values of HDT (36 days and 18 days respectively) and their removals of BOD and COD were the same (76% and 60%, respectively). The Beira Rio WSPS, was the most efficient verified in relation to solids and ammonia, proving the great influence of the operational variables such as HDT and applied surface organic loadings on the performance of pond series. Although the treatment plants have reached efficiencies of thermotolerant coliforms around 99,999%, the concentrations in the final effluent can be considered very high for launching in aquatic bodies, particularly those produced by Jardim Lola 1 and Jardim Lola 2 series

Health variables and gill morphology in the tropical fish Astyanax fasciatus from a sewage-contaminated river

The relative condition factor (Kn), gonadosomatic index (GSI), selected hematological variables and gill morphology of the fish Astyanax fasciatus were analyzed in two sites (site I was unpolluted and site 2 was polluted with untreated domestic sewage) of a tropical river (Camanducaia river, São Paulo State, Brazil). The relationship between the body mass (M-B) and the standard length (L-S) of A. fasciatus from both sites was M-B = 0.00799 L-S(3.51843). Tyhe Kn values from both the males and females were significantly higher in site 2. The mean corpuscular hemoglobin and mean corpuscular hemoglobin concentration were higher in females from site 2. Gill tissue anomalies and gill parasites were rare in fish from both sites; however, the number of chloride cells was significantly higher in fish from site 1. A. fasciatus presents high capacity to live in ion-poor and soft water and is able to compensate for environmental changes caused by untreated domestic sewage discharges. (c) 2004 Elsevier B.V. All rights reserved.

Microbiological and physicochemical treatments applied to metallurgic industry aiming water reuse

Estudou-se o reuso de água de um sistema composto por estação de tratamento de esgoto (ETE) com aeração prolongada e lodo ativado, e em uma estação compacta de tratamento de água (ECTA) de uma indústria metalúrgica. Os processos para obtenção da água de reuso foram: microbiológico e físico-químico. O esgoto doméstico foi bombeado para a ETE, onde houve formação de flocos biológicos e água clarificada. Avaliou-se a eficiência do processo microbiológico da ETE mediante a remoção de demanda bioquímica de oxigênio (DBO), demanda química de oxigênio (DQO) e sólidos sedimentáveis (SS). A eficiência do processo físico-químico de clarificação e desinfecção foi avaliada mediante análises de pH, turbidez, cor, contagem de bactérias heterotróficas aeróbias, cloro livre, dureza, alcalinidade, cloretos, sulfatos, sólidos totais dissolvidos (STD). Na água de reuso além desses parâmetros avaliou-se a toxicidade aguda ao microcrustáceo Daphnia similis.

An evaluation into the potential of biological processing for the removal of metals from sewage sludges

The use of sewage sludge in agricultural land as a means of sludge disposal and recycling has been shown to be economical and suitable because of the presence of nutrients such as nitrogen and phosphorus. However, municipal sludges often contain high quantities of toxic metals and other compounds that must be removed for its safe use in agricultural soils. The biological leaching of metals from sewage sludges has been shown to be a promising technique for metal detoxifying in such complex matrix. The process efficiency is dependent on several physico-chemical parameters, such as total solids concentration, metal forms, pH-ORP, and temperature. Scale-up of the process has not yet been defined and is still pursuing the correct operational design. Current research involving the bioleaching of metals from sewage sludge and its application to land, which affects soil physical properties, are presented and discussed.

Cogasification of solid fuels

High efficiency gas turbine based systems, utility deregulation and more stringent environmental regulations strongly favor the use of natural gas over coal and other solid fuels in new electricity generators. Solid fuels could continue to compete, however, if a low cost gasifier fed by low cost feedstocks can be coupled with a gas turbine system. We examine on-site gasification of coal with other domestic fuels in an indirectly heated gasifier as a strategy to lower the costs of solid fuel systems. The systematics of gaseous pyrolysis yields assembled with the help of thermal measurement data and molecular models suggests blending carbonaceous fuels such as coal, coke or char with oxygenated fuels such as biomass, RDF, MSW, or dried sewage sludge. Such solid fuel blending can, with the help of inexpensive catalysts, achieve an optimum balance of volatiles, heating values and residual char thus reducing the technical demands upon the gasifier. Such simplifications should lower capital and operating costs of the gasifier to the mutual benefit of both solid fuel communities.

Tratamento de esgoto sanitário utilizando reatores anaeróbios operados em bateladas sequenciais (escala piloto)

The performances of two anaerobic sequencing batch reactors (1.2 m 3) containing biomass immobilized in inert support and as granular sludge in the treatment of domestic sewage from the Campus of São Carlos-University of São Paulo were evaluated. The experimental phase lasted seventy days. During this period, the reactors presented quite similar performances in respect to COD and total suspended solids removal, achieving average efficiencies of approximately 60% and 75%, respectively. The analysis using molecular biology techniques on biomass samples taken at 35 th and 70 th showed differences in the bacterial community in the reactors indicating that the type of biomass immobilization selected the populations differently. A higher similarity was found for the Archaea domain probably because these microorganisms utilize specific substrates formed at the end of the anaerobic process.

Adubação mineral, esterco de curral e lodo de esgoto no desenvolvimento inicial do cafeeiro

Conselho Nacional de Desenvolvimento Científico e Tecnológico (CNPq)

Parâmetros químicos da solução de um solo fertilizado com lodo de esgoto em bananeiras irrigadas

Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)